static electricity and charge...
TRANSCRIPT
Safety Engineering
-Static Electricity and Charge Accumulation-
Conductive– A material with a low electrical resistance, electrons flow
easily across the surface or through the bulk of thesematerials and having a volume resistively equal or lowerthan 104Ω∙m
Dissipative– A material incapable or retaining a significant amount of
electrostatic charge when in contact with earth and having avolume resistivity higher than 104Ω∙m but equal to or lowerthan 109Ω∙m measured at ambient temperature and 50%relative humidity.
Non-conductive– A material prevent or limit the flow of electrons across its
surface or through its volume. Non-conductive materialshave a high electrical resistance and are difficult to groundand having a volume resistivity higher than 109Ω ∙ m
Definitions - Types of materials 2
• Generation of Spark Discharges.
– Charge accumulation at a conductive object.
– Field strength exceeds the electric strength of the ambient atmosphere.
• Ignitability--gases, vapors, dusts
• Energy transfer--up to 10,000 mJ
Types of discharges 3
• Discharging of static electricity between two conductors.
Spark Discharge
• Generation of Brush Discharges
– Conductive electrode moves towards a charged nonconductive object.
• Nonconductive lining or surface must have a breakdown voltage greater than 4 kV and a thickness greater than 2 mm.
• Nonconductive coating can be a layer of the powdered solid.
• Ignitability--gases, vapors
• Energy transfer--up to 4 mJ
4
Brush Discharge
Types of discharges
5
• Generation of Propagating Brush Discharge
– Bipolar charging of the high resistivity material (non conducting) that is lining another conductor.
– Field strength exceeds the electric strength of the high resistivity material. Non conducting lining must have breakdown voltage greater than 4 kV
• Ignitability--gases, vapors, dusts
• Energy transfer--up to 100,000 mJ
• Major contributor to static electricity ignitions.
Propagating Brush Discharge
Types of discharges
• Generation of Cone Discharge.– Vessels larger than 1 m3.– Relatively fast filling rate, greater
than 0.5 kg/s.– High resistivity (>1010Ωm) bulk
product, larger than 1 mm diameter.
– Charge accumulation in the bulk product.
– Field strength exceeds the electric strength of the ambient atmosphere.
• Ignitability--gases, vapors, dusts• Energy transfer--up to 1000 mJ
6
Cone Discharge
Types of discharges
Type of Discharge Energy transfer Ignitability
Spark < 10 000 mJ gases, vapor, dusts
Brush < 4 mJ gases, vapor
Propagating Brush < 100 000 mJ gas, vapor, dusts
Cone < 1 000 mJ gas, vapor, dusts
Corona < 0.1 mJ some gases with
low MIE
Ignitability of discharges 7
Whenever two dissimilar materials come in contact, electrons move from one surface to the other. As these materials are separated and more electrons remain on one surface than the other, one material takes on a positive charge and the other a negative charge.
Mechanisms for Charge Accumulation:
– Contact and Frictional
– Double layer
– Induction
– Transport
Charge Accumulation 8
• Dust transport– e.g. pneumatic transport of powders/solids
• Pouring powders– e.g. pouring solids down chutes or troughs
• Gears and belts– e.g. transporting charges from one surface to another
Charge Accumulation 9
Contact and Frictional Charging
Double layer charging
Caused by friction and movement at interfaces on a microscopic scale.
– Liquid-liquid
– Solid-liquid
– Solid-solid
– Gas-liquid
– Gas-solid
When an isolated conductor is subject to a electric field a chargepolarity develops on the object. If the object is grounded then thecharges closest to the grounding source flows away leaving the bodywith a net charge of opposite sign.
Charge Accumulation 10
Induction charging
Charging by Transport
• Results from a charged dust, liquid or solid particles settling onto a surface and transporting their charges to this new surface.
• The rate of charge accumulation is a function of the rate of transportation.
Many fluid handling operationscan generate static electricity.This becomes a problem whennon conducting pipes (glass orTeflon lined) are used withoutadequate bonding.
Charging by Transport 11
Fluid handling operations
Splash Filling
• When non conducting fluids (or solids) free fall through air they pick up a significant static charge.
• When there is spraying or splashing static electricity can build up.
• This can be a source of sparks
• When fluid flows into a vessel it carriesa charge with it which can build up inthe tank if the tank is not properlygrounded.
• Routine inspection of groundingminimizes the change for fire orexplosion due to a spark discharge fromthe charged tank.
Charging by Transport 12
Fluid flow into vessels
When a liquid or solid isflowing, there is a transfer ofelectrons from one surface toanother as they flow past eachother.
Charging by Transport 13
Streaming current
The time required for a chargeto dissipate by leakage.
Charging by Transport 14
Relaxation time
1 mho/centimeter [mho/cm] = 100 siemens/meter [S/m]
Example:toluene- poor conductivity- relaxation time: 21 s
For flow through a non conducting pipe(glass, Teflon lined) a voltage drop candevelop from flowing liquid.
Charging by Transport 15
Electrostatic Voltage Drops
Charges can accumulate as a result of streaming current
Assuming constant streaming current
Solid geometries are almost always ill defined, so need to be based onempirical calculations. Solid processing operations have differentempirically determined charge capacities.
Q = Charge Capacity X Charge Rate X time coulombs kg
Q skg s
Charging by Transport 16
Accumulated charge from solid handling
Process Charge Capacity (coulombs/kg)
Sieving 10-9 to 10-11
Pouring 10-7 to 10-9
Grinding 10-6 to 10-7
Sliding down incline 10-5 to 10-7
Pneumatic transport 10-5 to 10-7
Capacitance 17
Capacitance is the ability of a body to store an electrical charge.Capacitance for a sphere for plates
Object Cpacitance (farad)Small scoop 5 x 10-12
Bucket 10 x 10-12
Barrel 100 x 10-12
Person 200 x 10-12
Automobile 500 x 10-12
Tank Truck 1000 x 10-12
Capacitance of Various Objects
Static Energy Stored
• Determine the capacitance, C, of the object or container contents, expressed in farads or coulombs per volt.
• Determine the accumulated charge, Q, expressed in coulombs
• Compute accumulated energy, E, expressed in J or mJ.
• Compare to the MIE of the dust or vapor.
Calculations 18
Determine the potential hazard of pneumatically transporting a dry powder (dry powder with a particle size greater than 1 mm) at a rate of 30,000 kg/hr into a metal vessel which has a volume of 70 m3.
Given: The powder has a bulk density of 600 kg/m3; the vessel has a spherical geometry; 70 m3 of powder is charged into the vessel. The powder is flammable with a MIE of 20 mJ.
Example – Solids handling
• Determine radius of sphere:
• Calculate capacitance:
113 333 3 70
2.54 4
V mr m
0
12 10
4
= 1 for air (Table 7-1) Spark jumps across air gap
4 (1) 8.85 10 2.5 2.83 10
r
r
C r
coul coulC mvolt m volt
Example – solids handling - solution 19
(Tab. slide15)
• Determine mass fed:
• Calculate charge accumulated (Tab. slide 17, pneumatictransport):
3
370 600 42,000
kgFeed m kg
m
510 42,000 0.42coulQ kg coulkg
Example – solids handling – solution (cont.) 20
• Calculate energy:
• This is much greater than the MIE of the powder. If there is sufficient air this would be very hazardous.
• This is the total charge that could go into vessel while filling. Multiple discharges would occur, certainly there would be conical pile discharges (unless grounded).
228
10
0.423.1 10
2 2 2.83 10
coulQE J
coulCvolt
• Charge buildup is always possible when you have moving fluids or solids. The potential for discharge is always present.
• We can eliminate sparks if we ensure that all parts of the system are connected with a conductor.
• Historically there was little problem when piping was all copper, stainless steel or iron. The problem comes when pipes or vessels are glass or Teflon lined or made from polymers or connected with non-conducting gaskets.
• There has always been a problem when you are pouring either liquid or a solid through an open space i.e., a filling operation.
Elimination of Charge Accumulation 21
Bonding and Grounding
• Bonding– Is the connection of a
conducting wire between two or more objects.
– The voltage difference between the two objects is reduced to zero, however they may have a voltage difference relative to ground or another non connected object
• Grounding– Is the connection of a
conducting wire between a charged object and the ground.
– Any charge accumulated in the system is drained off to ground.
Elimination of Charge Accumulation 22
Bonding and Grounding
Elimination of Charge Accumulation 23
Bonding
Elimination of Charge Accumulation 24
Grounding
Elimination of Charge Accumulation 25
Grounding
Elimination of Charge Accumulation 26
Grounding
Elimination of Charge Accumulation 27
Grounding
• Glass and plastic lined vessels are grounded using tantalum inserts or a metal probe.
• This is less effective if fluid has low conductivity.
Elimination of Charge Accumulation 28
Grounding Glass-lined Vessels
• To eliminate the static charge that builds up from a fluid free falling through air, a dip leg is used. Note hole to prevent back siphoning.
• An angle iron can also be used so fluid runs down the angle iron instead of free falling.
Elimination of Charge Accumulation 29
Dip Legs to Reduce Splash Filling
Following are a series of case studies of accidents that actually happen at BASF and Dow and shared with the SACHE Chemical Process Safety Workshop participants.
Case Studies from a production plant 30
• Situation– A non-conductive bulk product is
fed out of 25 kg PE-bags in a vessel, in which a flammable liquid is being stirred. During shaking of the the just empty bag an ignition occurred.
• Cause– All handling of non-conductive
solids or bulk products may generate static electricity. Due to contact charging of the sliding bulk product, both the bulk product and non conducting package materials became charged. Brush discharges form the surface of the bad ignited the vapor/air mixture.
• Precaution– Either fill into a closed, inerted
vessel or avoid charge generation.
Case Studies from a production plant 31
Solids Filling Operation
• Situation– An operator filled a non-conductive
bulk product out of 25 kg PE-bags in a solvent free mixer. Exhaust system operated. All equipment grounded, the floor was dissipative, the operator wore dissipative footwear. During pouring the product in the reaction vessel explode.
• Cause– The plastic wrap that held the sacks
on the pallet was on the floor and the operator was standing on it. This allowed a static charge to build up in him.
• Precaution– Always guarantee ground
connection.
Case Studies from a production plant 32
Operator
• Situation– A ball-valve is installed in a waste
gas collecting system. During usual production an explosion occurred; the pipe system was destroyed.
• Cause– A valve consists of conductive and
non-conductive parts. Conveying of dust suspensions or droplets may generate charge accumulation on the ball and/or shaft if not bonded to the grounded housing. Spark discharge from charged ball to housing caused explosion.
• Precaution– Guarantee ground connection of
conductive equipment.
Case Studies from a production plant 33
Valve
• Situation– A pure liquid was filled in a steel drum
with an inner plastic liner. To avoid splash filling a short funnel was inserted in the spout. The nozzle, the drum and the weighing machine were all grounded. Despite having an exhaust system there was an explosion during drum filling.
• Cause– Electrostatic charge generation at the
surface of the non-conductive coating cannot be transferred. The funnel had sufficient capacitance was insulated from the ground by the PE lined filler cap. Spark discharge from funnel caused explosion.
• Precautions– Guarantee ground connection of all
conductive equipment.
Case Studies from a production plant 34
Lined metal drum filling
Example – Fluid Handling
• Determine the voltage developed between a charging nozzle and a grounded tank and the charge accumulated during the filling process at 150 gpm.
Example – Fluid Handling (cont.)
• Additional information:
– Non conducting hose length 20 ft
– Hose diameter 2 in.
– Liquid conductivity 10-8 mho/cm
– Liquid diffusivity 2.2x10-5 cm2sec-1
– Dielectric constant 25.7
– Density 0.88 g/cm3
– Viscosity 0.60 centipoise
– MIE 0.10 mJ
Example – fluid handling - solution
• Procedure
• Calculate voltage drop using V=IsR (Eq. 7-17)
• Calculate R using Eq. 7-18
• Calculate Is using Eq. 7-12 or 7-14
• Calculate Q using Q=Ist
• Calculate E=(QV/2)
• Compare to MIE
Example – fluid handling – solution (cont.)
Calculate the Resistance
222 2
9
82
12 . 2.54(20 ) 610.
3.541 . 20.3.
6103.00 10
10 20.3C
in cmL ft cmft in
cmA r in cmin
L cmR
A cmcm
Example – fluid handling – solution (cont.)
• Determine type of flow (laminar or turbulent)
3 2
2 2
3
3
150 144 1minmin 15.37.48 601 .
2 15.3 0.887750
Re 348,0000.60
Hence Turbulent
gallonft in ft
usgal ft sin
ft gin
du s cpcm
ft gcp ins cm
Example – fluid handling – solution (cont.)
• Calculate the streaming current:
14
50
8
2-5 5 -5 -5
14
14
25.7 8.85 1022.7 10 (Eq. 7-16)
10
= 2.2 10 22.7 10 = 7.07 10 = 2.78 10 . (Eq. 7-15)
5.89 10 (Eq.7-14)
5.89 10
r
C
m
rs
s
scm s
mhocm
cmD s cm ins
amp d uI
ftvolt
s
ampI
7
-5
2 153 25.7 0.1
1.66 102.78 10
ftin volt
samp
ft involts
Example – fluid handling – solution (cont.)• Calculate the voltage drop, accumulated charge and
energy:
7 9
5 5
5
(1.66 10 ) 3.00 10 498 (Eq. 7-17)
Determine fill time
300 60min 120
150min
Determine accumulated charge
1.66 10 120 1.99 10
Determine Energy
1.99 10
2
s
s
V I R amp volts
sgalt s
gal
Q I t amp s coulomb
couloQVE
4984.9
2
This is greater than the MIE, so there is a fire or explosion hazard
mb voltmJ
Static electricity & charge accumulation
• Definitions
• Types of discharges
• Mechanisms of charge accumulation– fluid systems - Streaming current
– Solids handling
• Balance of charges
• Bonding and grounding
• Case studies
Balance of Charges
• When you have a vessel that has multiple inputs and outputs, you can determine the charge accumulation by a charge balance.
• Consider streaming currents in, charges carried away by flows going out, and charge loss due to relaxation.
Charge Balance
, ,1 1
,1
,1
where
is the current coming into the vessel
is the current flowing out of the vessel
is the charge loss due to relaxation
is the relaxation ti
n m
s si in j outi j
n
s i ini
m
s j outj
dQ QI I
dt
I
I
Q
me
Charge Balance
,
The charge flowing out of the vessel depends
on the charge already in the tank
where
is the rate of discharge through outlet
is the container or tank volume
is the total char
j
s j outC
j
C
FI Q
V
F j
V
Q
ge in the tank
Charge Balance
,1 1
,
Hence the charge balance becomes
If flows, , streaming currents, , and relaxation times, ,
are constant, then this is a linear di
n mj
s i ini j C
j s i in
FdQ QI Q
dt V
F I
, ,
1 10
1
1 1
fferential equation that has
the solution:
where
1
1 1
Ct
n n
s s mi in i inji i
m mj Cj j
j jC C
Q A Be
I IF
A B Q CVF F
V V
Charge Balance
• This relationship is used to determine the charge developing in the tank as a function of time relative to an initial charge of Q0.
• The capacitance of the vessel is calculated as before (typically assume equivalent spherical vessel).
• The static energy stored in the vessel is then calculated from E=Q2/2C.
• Examples 7-9 and 7-10 demonstrate using this relationship.
Static electricity & charge accumulation
• Definitions
• Types of discharges
• Mechanisms of charge accumulation– fluid systems - Streaming current
– Solids handling
• Balance of charges
• Bonding and grounding
• Case studies